- InChI
- InChI=1S/C6H12O/c1-3-5-6-7-4-2/h4H,2-3,5-6H2,1H3
- InChI Key
- UZKWTJUDCOPSNM-UHFFFAOYSA-N
- Formula
- C6H12O
- SMILES
- C=COCCCC
- Molecular Weight1
- 100.16
- CAS
- 111-34-2
- Other Names
-
- 1-(ETHYNYLOXY)BUTANE
- 1-(Vinyloxy)-butane
- 1-(ethenyloxy)butane
- 1-(vinyloxy)butane
- 1-Butoxyethylene
- 1-vinyloxybutane
- BVE
- Butoxyethylene
- Ethenyl n-butyl ether
- Ether, butyl vinyl
- NSC 8264
- Vinyl butyl ether
- Vinyl n-butyl ether
- butoxyethene
- butyl vinyl ether
- n-Butyl vinyl ether
- n-C4H9OCH=CH2
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3954 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | [-3860.20; -3857.00] | kJ/mol |
|
| ΔcH°liquid | -3860.20 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -3857.00 ± 0.80 | kJ/mol | NIST |
| ΔfG° | -17.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-182.40; -179.20] | kJ/mol |
|
| ΔfH°gas | -179.20 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -182.40 | kJ/mol | NIST |
| ΔfH°liquid | [-219.00; -215.80] | kJ/mol |
|
| ΔfH°liquid | -215.80 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -219.00 ± 0.80 | kJ/mol | NIST |
| ΔfusH° | 11.20 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [34.00; 36.70] | kJ/mol |
|
| ΔvapH° | 36.24 | kJ/mol | NIST |
| ΔvapH° | 36.59 ± 0.23 | kJ/mol | NIST |
| ΔvapH° | 36.60 | kJ/mol | NIST |
| ΔvapH° | 36.70 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 36.50 | kJ/mol | NIST |
| ΔvapH° | Outlier 34.00 ± 3.00 | kJ/mol | NIST |
| IE | 8.90 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.89 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.947 | Crippen Calculated Property | |
| McVol | 96.970 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 3200.00 ± 250.00 | kPa | NIST |
| ρc | 261.11 ± 12.02 | kg/m3 | NIST |
| Inp | [671.00; 695.00] |
|
|
| Inp | 695.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 695.00 | NIST | |
| I | 858.00 | NIST | |
| Tboil | [366.00; 367.10] | K |
|
| Tboil | 367.00 | K | NIST |
| Tboil | 366.00 | K | NIST |
| Tboil | 367.10 | K | NIST |
| Tc | 540.50 ± 2.00 | K | NIST |
| Tfus | 173.98 | K | Relay (1.0) Calculated Property |
| Vc | 0.365 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [168.44; 221.40] | J/mol×K | [355.98; 523.97] |
|
| Cp,gas | 168.44 | J/mol×K | 355.98 | Joback Calculated Property |
| Cp,gas | 178.00 | J/mol×K | 383.98 | Joback Calculated Property |
| Cp,gas | 187.26 | J/mol×K | 411.98 | Joback Calculated Property |
| Cp,gas | 196.22 | J/mol×K | 439.98 | Joback Calculated Property |
| Cp,gas | 204.90 | J/mol×K | 467.97 | Joback Calculated Property |
| Cp,gas | 213.29 | J/mol×K | 495.97 | Joback Calculated Property |
| Cp,gas | 221.40 | J/mol×K | 523.97 | Joback Calculated Property |
| Cp,liquid | 231.80 | J/mol×K | 298.15 | NIST |
| η | [0.0002119; 0.0029205] | Pa×s | [177.85; 355.98] |
|
| η | 0.0029205 | Pa×s | 177.85 | Joback Calculated Property |
| η | 0.0013797 | Pa×s | 207.54 | Joback Calculated Property |
| η | 0.0007864 | Pa×s | 237.23 | Joback Calculated Property |
| η | 0.0005079 | Pa×s | 266.92 | Joback Calculated Property |
| η | 0.0003580 | Pa×s | 296.60 | Joback Calculated Property |
| η | 0.0002690 | Pa×s | 326.29 | Joback Calculated Property |
| η | 0.0002119 | Pa×s | 355.98 | Joback Calculated Property |
| ΔvapH | [29.60; 36.10] | kJ/mol | [318.50; 367.10] |
|
| ΔvapH | 36.10 | kJ/mol | 318.50 | NIST |
| ΔvapH | 35.20 ± 0.20 | kJ/mol | 357.00 | NIST |
| ΔvapH | 32.50 ± 0.20 | kJ/mol | 357.00 | NIST |
| ΔvapH | 29.60 ± 0.20 | kJ/mol | 357.00 | NIST |
| ΔvapH | 31.58 | kJ/mol | 367.10 | NIST |
| ρl | [758.80; 780.20] | kg/m3 | [298.15; 313.15] |
|
| ρl | 780.20 | kg/m3 | 298.15 | Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether |
| ρl | 769.00 | kg/m3 | 303.15 | Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether |
| ρl | 774.10 | kg/m3 | 303.15 | Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether |
| ρl | 763.90 | kg/m3 | 308.15 | Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether |
| ρl | 768.20 | kg/m3 | 308.15 | Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether |
| ρl | 758.80 | kg/m3 | 313.15 | Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether |
| ρl | 763.30 | kg/m3 | 313.15 | Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [274.58; 389.11] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54615e+01 | |||
| Coefficient B | -3.51136e+03 | |||
| Coefficient C | -4.31680e+01 | |||
| Temperature range, min. | 274.58 | |||
| Temperature range, max. | 389.11 | |||
| Pvap | 1.33 | kPa | 274.58 | Calculated Property |
| Pvap | 2.94 | kPa | 287.31 | Calculated Property |
| Pvap | 6.00 | kPa | 300.03 | Calculated Property |
| Pvap | 11.43 | kPa | 312.76 | Calculated Property |
| Pvap | 20.57 | kPa | 325.48 | Calculated Property |
| Pvap | 35.17 | kPa | 338.21 | Calculated Property |
| Pvap | 57.53 | kPa | 350.93 | Calculated Property |
| Pvap | 90.49 | kPa | 363.66 | Calculated Property |
| Pvap | 137.51 | kPa | 376.38 | Calculated Property |
| Pvap | 202.62 | kPa | 389.11 | Calculated Property |
| Pvap | [1.31e-04; 3086.33] | kPa | [181.15; 536.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.18610e+01 | |||
| Coefficient B | -7.10617e+03 | |||
| Coefficient C | -9.96430e+00 | |||
| Coefficient D | 7.13053e-06 | |||
| Temperature range, min. | 181.15 | |||
| Temperature range, max. | 536.00 | |||
| Pvap | 1.31e-04 | kPa | 181.15 | Calculated Property |
| Pvap | 0.02 | kPa | 220.58 | Calculated Property |
| Pvap | 0.67 | kPa | 260.01 | Calculated Property |
| Pvap | 7.05 | kPa | 299.43 | Calculated Property |
| Pvap | 38.90 | kPa | 338.86 | Calculated Property |
| Pvap | 141.40 | kPa | 378.29 | Calculated Property |
| Pvap | 387.84 | kPa | 417.72 | Calculated Property |
| Pvap | 875.73 | kPa | 457.14 | Calculated Property |
| Pvap | 1725.20 | kPa | 496.57 | Calculated Property |
| Pvap | 3086.33 | kPa | 536.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Butane, 1-(ethenyloxy)-.
Mixtures
- Acetic acid ethenyl ester + Butane, 1-(ethenyloxy)-
- Butane, 1-(ethenyloxy)- + Acetic acid, hexyl ester
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
- Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.